Supercritical CO2 Processing for Submicron Imaging of

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Chem. Mater. 2000, 12, 41-48

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Supercritical CO2 Processing for Submicron Imaging of Fluoropolymers Narayan Sundararajan, Shu Yang, Kenji Ogino,† Suresh Valiyaveettil,‡ Jianguo Wang,§ Xinyi Zhou,| and Christopher K. Ober* Department of Materials Science and Engineering, Cornell University, Ithaca, New York 14853

Sharon K. Obendorf Department of Textiles, Cornell University, Ithaca, New York 14853

Robert D. Allen IBM Almaden Research Center, 650 Harry Road, San Jose, California 95120 Received April 27, 1999. Revised Manuscript Received November 2, 1999

To keep pace with the ever-shrinking feature sizes required in the microelectronics industry, suitable developers with high diffusivities, selectivity, and adjustable solvating power are required. Supercritical fluid (SCF) CO2 possesses many of the above unique properties and could serve as an “environmentally responsible” alternative developer to aqueous base. In this study, the high solubility of fluorinated block copolymers in supercritical CO2 and the selectivity of supercritical CO2 to both polarity changes and the molecular structure of the polymer were utilized to develop an environmentally friendly lithographic process. Polymers with acid-cleavable tetrahydropyranyl groups and supercritical CO2 soluble, fluoro-side-chain-containing methacrylate groups were synthesized with varying volume fractions of the components, and their solubilities in supercritical CO2 were characterized. Chemical amplification was used to effect the polarity change leading to the solubility difference in supercritical CO2, and the lithographic performance was evaluated. Important parameters such as sensitivity, contrast, and resolution were investigated, and 0.2 µm features using supercritical CO2 development were demonstrated.

Introduction Supercritical fluid (SCF) technology has been gaining considerable attention over the last two decades in the area of polymer synthesis and processing.1 This has been due to the unique properties of supercritical fluids, such as their high diffusivities comparable to those of gases, their liquid-like densities, and also the ability to control their densities and hence their solvating powers by the simple manipulation of pressure and temperature conditions. SCF technology has been widely applied in the food and pharmaceutical industries to use in such techniques as supercritical fluid chromatography and extraction of toxic compounds from wastewater. Carbon dioxide is rapidly becoming a very attractive candidate among the supercritical fluids for replacing traditional liquid organic solvents in various applications such as coatings, separations, polymerization, and † Current address: Tokyo University of Agriculture and Technology, Material Systems and Engineering, 2-24-16 Nakacho, Koganei, Tokyo 184, Japan. ‡ Current address: Department of Chemistry, National University of Singapore, Lower Kent Ridge Road, Singapore 119 260. § Current address: Corning Incorporated, Research Dept, Polymer Core Technology, HP-ME-01-033-B7, Corning, NY 14831. | Current address: Advanced Micro Devices, One AMD Place, P.O. Box 3453, M/S 117, Sunnyvale, CA 94088. (1) McHugh, M. A.; Krukonis, V. J. Supercritical Fluid Extraction Principles and Practice; Butterworth: Stoneham, MA, 1994.

antisolvents. Though SCF CO2 has been found to be a very good solvent for small molecules, it acts as an extremely poor solvent for polymers. Very few classes of polymers have appreciable solubility in SCF CO2 at the conditions T < 100 °C and P < 5000 psi.2 In terms of their solubility in CO2, polymers have been classified as CO2-philic and CO2-phobic. While conventional hydrophilic or lipophilic polymers are relatively insoluble in CO2, fluoropolymers and silicon-containing polymers fall into the CO2-philic category. For some time, fluorocopolymers have been known to be soluble in SCF CO2, and in fact, a variety of acrylic and styrene fluoropolymers have been synthesized in SCF CO2 using homogeneous free radical polymerization. Statistical copolymers containing up to 50 mol % of the hydrocarbon moiety with a second fluoropolymer component have been found to be soluble in SCF CO2.3,4 The mechanism of solubility of polymers in SCF CO2 has been the subject of much research in recent years. Some of the factors which have been identified as important parameters are the specific solute-solvent interactions between the polymers and CO2, solute(2) DeSimone, J. M.; Guan, Z. Macromolecules 1994, 27, 5527-5532. (3) DeSimone, J. M.; Guan, X.; Elsbernd, C. S. Science 1992, 257, 945-947. (4) Guan, Z.; Combes, J. R.; Mencologlu, Y. Z.; DeSimone, J. M. Macromolecules 1993, 26, 2663-2669.

10.1021/cm9902467 CCC: $19.00 © 2000 American Chemical Society Published on Web 12/20/1999

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Figure 1. Scheme of the lithographic process showing both positive- and negative-tone imaging.

solute interactions, van der Waals interactions, Lewis acid-base interactions, the free volume and cohesive energy density of the polymer, and so forth.5-14 It has been found that the solubility of a polymer in SCF CO2 has a marked dependency on the structure of the polymer, including both the backbone and the side chain. Hence, manipulation of the polymer solubility in SCF CO2 is indeed possible by careful tailoring of the molecular structure. Solubility switching phenomena obtained by controlling the molecular structure of a polymer has been utilized for over two decades in the electronics industry, in the lithographic process used to pattern integrated circuits.15 The lithography process is shown schematically in Figure 1. In this process, a polymeric material is spun onto a substrate such as a silicon wafer to form a uniform coating. Then, the polymer is exposed to a source of photons, electrons, or X-rays through a mask which has the pattern information to be transferred. The mask allows the radiation to pass through previously defined areas. The polymer exposed to the radiation undergoes a chemical change (cross-linking, chainscission, or polarity change). The next step is the use of a solvent to selectively remove the exposed or the unexposed regions to successfully transfer the pattern onto the polymer layer. The polymer is called a positivetone resist if the exposed regions become more soluble in the solvent and a negative-tone resist if the opposite (5) Fried, J. R.; Li, J. J. Appl. Polym. Sci. 1990, 41, 1123-1131. (6) Kazarian, S. G.; Vincent, M. F.; Bright, F. V.; Liotta, C. L.; Eckert, C. A. J. Am. Chem. Soc. 1996, 118, 1729-1736. (7) Lepilleur, C.; Beckman, E. J.; Schonemann, H.; Krukonis, V. J. Fluid Phase Equilib. 1997, 134, 285-305. (8) Mertdogan, C. A.; Byun, H.-S.; McHugh, M. A.; Tuminello, W. H. Macromolecules 1996, 29, 6548-6555. (9) Mertdogan, C. A.; DiNoia, T. P.; McHugh, M. A. Macromolecules 1997, 30, 7511-7515. (10) O’Shea, K. E.; Kirmse, K. M.; Fox, M. A.; Johnston, K. P. J. Phys. Chem. 1991, 95, 7863-7867. (11) Shah, V. M.; Hardy, B. J.; Stern, S. A. J. Polym. Sci., Part B: Polym. Phys. 1986, 24, 2033-2047. (12) Shah, V. M.; Hardy, B. J.; Stern, S. A. J. Polym. Sci., Part B: Polym. Phys. 1993, 31, 313-317. (13) O’Neill, M. L.; Cao, Q.; Fang, M.; Johnston, K. P.; Wilkinson, S. P.; Smith, C. D.; Kerschner, J. L.; Jureller, S. H. Ind. Eng. Chem. Res. 1998, 37, 3067-3079. (14) Luna-Barcenas, G.; Mawson, S.; Takishima, S.; DeSimone, J. M.; Sanchez, I. C.; Johnston, K. P. Fluid Phase Equilib. 1998, 146, 325-337. (15) Thompson, L. F.; Willson, C. G.; Bowden, M. J. Introduction to Microlithography, 2nd ed.; American Chemical Society: Washington, DC, 1994.

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is true. It is very important that the solvent used for the image transfer has the ability to distinguish between very small areas of chemical differences in the polymer structure. Supercritical fluid CO2 could thus be envisioned as an “environmentally responsible” solvent for solventintensive processes in lithography such as the spincoating and development steps, wherein a polymer soluble in liquid CO2 could be coated directly using liquid CO2,16 exposed, and then developed using supercritical/liquid CO2. The initial experiments using SCF CO2 as a solvent for microelectronics applications were conducted by Taylor et al.17 They extracted unreacted siloxane compounds from an organic polymer matrix. From their work, a window of processing conditions for achieving 0.75-µm resolution for an X-ray-exposed lithography system was defined. Allen et al.18 used the selectivity of SCF CO2 based on molecular weight differences to study the effect of molecular weight on the glass transition and the dissolution rate of novolac resin and thereby on the lithographic performance. In addition to their selectivity based on molecular weight differences, SCF CO2 is also very sensitive to changes in the polarity of the polymer. Researchers at IBM and Phasex Corporation have used this concept in designing novel photoresists.19-21 They accomplished the polarity switch needed for the solubility change in SCF CO2 using the chemical amplification mechanism and demonstrated the solubility difference between the exposed and the unexposed regions of the polymeric photoresist film. A variety of fluoro- and silicon-containing polymers were tested in both positiveand negative-tone resist schemes where the film becomes more soluble in SCF CO2 after exposure and viceversa. Recently, our research group demonstrated the good contrast and excellent sensitivity of siliconcontaining block copolymers as SCF CO2 developable photoresists.22 Other applications of SCF CO2 in the area of microelectronics include surface cleaning and removal of the solvent remaining after processing and development. SCF CO2 drying was found to be very effective in the case of high aspect ratio features due to the very low surface tension of supercritical fluids. In this study, we utilized the high solubility of fluorinated block copolymers in SCF CO2 and the selectivity of this solvent to polarity changes and the molecular structure of a polymer to develop an environmentally friendly lithographic process. Polymers with acid-cleavable tetrahydropyranyl groups and SCF CO2 soluble perfluorinated methacrylate segments were synthesized with varying volume fractions of the components, and their solubilities in SCF CO2 were characterized. Chemical amplification was used to effect the polarity change leading to the solubility difference in (16) DeSimone, J. M. Proc. ACS Polym. Mater. Sci. 1998, 79, 290. (17) Ziger, D. H.; Wolf, T. M.; Taylor, G. N. AIChE J. 1987, 22, 1585-1591. (18) Allen, R. D.; Chen Rex, K. J.; Gallagher-Wetmore, P. M. Proc. SPIE 1995, 2438, 250-260. (19) Gallagher-Wetmore, P.; Ober, C. K.; Gabor, A. H.; Allen, R. D. Proc. SPIE 1996, 2725, 289-299. (20) Gallagher-Wetmore, P.; Wallraff, G. M.; Allen, R. D. Proc. SPIE 1995, 2438, 694-708. (21) Allen, R. D.; Wallraff, G. M. IBM Corp., Armonk, NY, 1997. U.S. Patent No. 5,665,527. (22) Ober, C. K.; Gabor, A. H.; Gallagher-Wetmore, P.; Allen, R. D. Adv. Mater. 1997, 9, 1039-1043.

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Figure 2. General scheme for synthesis of copolymers of tetrahydropyranyl methacrylate and fluorinated methacrylate using group-transfer polymerization.

SCF CO2, and the lithographic performance of these new fluoropolymers was evaluated. Important parameters such as sensitivity, contrast, and resolution were investigated, and 0.2 µm features using SCF CO2 development were demonstrated. Experimental Section Materials. Tetrahydrofuran (THF) (Aldrich) was freshly distilled from sodium/benzophenone under nitrogen before polymerization. The initiator methyl trimethylsilyl dimethylketene acetal {[(1-methoxy-2-methyl-1-propenyl)oxy]trimethylsilane, MTMS} (Aldrich) was distilled and stored under nitrogen. 2-Tetrahydropyranyl methacrylate (THPMA) was synthesized as described in the literature.23 The commercially available monomers 1H,1H-perfluoro-n-butyl methacrylate (F3MA, Lancaster) and 1H,1H-perfluorooctyl methacrylate (F7MA, Lancaster) were first purified by stirring with CaH2 for 24-48 h, followed by vacuum-distillation into a cold trap. The monomer was transferred to a monomer reservoir under nitrogen and stored at -20 °C. The catalyst tetrabutylammonium (TBA) biacetate was prepared as described in the literature24 and was dissolved in freshly distilled THF to give a 0.04 M solution. A small amount of water (6 molar equiv) was added to facilitate dissolution. Synthesis of Copolymers of Tetrahydropyranyl Methacrylate (THPMA) and Fluorinated Methacrylates. A detailed description of the synthetic procedures used is published in a separate paper.25 A general reaction scheme for the synthesis of block copolymers of tetrahydropyranyl (THP) methacrylate and fluorinated methacrylates is shown in Figure 2. In this procedure, THPMA was always polymerized first. Methanol or hexane was used as a precipitation solvent. A. Synthesis of Block Copolymers of THPMA and 1H,1HPerfluorobutyl Methacrylate (F3MA): A typical example for the synthesis of THPMA-b-F3MA (F3-4) block copolymers is (23) Taylor, G. N.; Stillwagon, L. E.; Houlihan, F. M.; Wolf, T. M.; Sogah, D. Y.; Hertler, W. R. Chem. Mater. 1991, 3, 1031-1040. (24) Patrickios, C. S.; Hertler, W. R.; Abbott, N. L.; Hatton, T. A. Macromolecules 1994, 27, 930-937. (25) Yang, S.; Wang, J.-G.; Ogino, K.; Valiyaveettil, S.; Ober, C. K. Chem. Mater., submitted.

Table 1. Characteristics of THPMA-b-F3MA Block Copolymers THPMA/F3MA (% v/v)

molecular weighta

sample in feed in polymer Mn/103 Mw/103 F3-1 F3-2 F3-3 F3-4 F3-5 F3-6 F3-7 F3-8 F3-9 F3-10

75/25 75/25 65/35 50/50 50/50 50/50 50/50 33/67 33/67 20/80

89/11 78/22 68/32 62/38 54/46 49/51 47/53 44/56 38/62 29/71

8.52 7.26 7.43 6.1 5.51 7.89 6.55 4.19 5.9 5.43

8.88 8.18 7.93 6.89 6.94 8.96 7.27 4.82 6.9 6.08

polydispersity yield Mw/Mn (%) 1.04 1.13 1.09 1.13 1.26 1.14 1.11 1.15 1.17 1.12

79 99 93 56 89 82 93 62 74 72

a Measured with GPC using refractive index detector, and PMMA as calibration standard.

described below: After 8 mL of THF was distilled into the reactor, 67 µL (0.33 mmol) of MTDA and 8.3 µL (0.34 × 10-3 mmol) of TBA biacetate solution were added. After 5 min, 1.35 mL (8.32 mmol) of THPMA was added over a period of approximately 3 min. The temperature of the solution rose from 22.5 to 40.0 °C. With 30 min of stirring, the temperature was cooled back to room temperature. After the mixture was stirred for an additional 30 min, 1.35 mL (7.05 mmol) of F3MA was added all at once. The temperature did not change over approximately 2 min and then suddenly increased and reached a maximum of approximately 41.0 °C in 1 min. A milky solution was observed in the initial 2 or 3 s during the temperature rise. The reaction was quenched with approximately 1 mL of methanol and poured into 200 mL of methanol after stirring for 2 h. After filtration and washing with hexane, the polymer was air-dried at room temperature and then dried 12 h in a vacuum oven at room temperature. Block copolymer was obtained with a yield of 2.7 g (∼82%). Table 1 shows the characteristics of THPMA-b-F3MA. B. Synthesis of Block Copolymers of THPMA and 1H,1HPerfluorooctyl Methacrylate (F7MA). A typical procedure for the synthesis of THPMA-b-F7MA (50:50 vol %) is given below: After 10 mL of THF was distilled into a reactor, 56 µL (9.34 mmol) of MTDA and 10.4 µL of TBA biacetate solution

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Table 2. Characteristics of THPMA-b-F7MA Block Copolymers THPMA/F3MA (% v/v)

molecular weighta

sample in feed in polymer Mn/103 Mw/103 F7-1 F7-2 F7-3 F7-4 F7-5 F7-6 F7-7 F7-8

75/25 50/50 33/66 40/60 33/66 27/73

78/23 50/50 46/54 45/55 37/63 34/66 32/68 23/77

8.47 8.85 10.1 5.2 8.2 8.95 6.61 7.7

9.4 9.5 11.11 5.67 8.77 9.54 7.14 8.32

polydispersity yield Mw/Mn (%) 1.11 1.07 1.1 1.09 1.07 1.07 1.08 1.08

89 89 71 92 85 92

a Measured with GPC using refractive index detector, and PMMA as calibration standard.

were added. After 5 min, 1.5 mL (9.34 mmol) of THPMA was added over 3 min. The temperature rose from 22.5 to 38.6 °C. With 30 min of stirring, the temperature was cooled back to room temperature. After the mixture was stirred for an additional 30 min, 1.5 mL (4.49 mmol) of predistilled F7MA was added to the living poly-THPMA solution. The temperature of the solution increased up to 28 °C within 1 min, and the solution was left stirring for another 2 h. The color of the solution changed to light blue and with time to pale yellow. The viscosity of the solution also seemed to change during the polymerization. The mixture was stirred for another 5 h, and the polymer was then precipitated into 250 mL of methanol. The solid polymer was filtered after 2 h of stirring and dried under vacuum at room-temperature overnight. Table 2 shows the characteristics of THPMA-b-F7MA copolymers. C. Synthesis of a Random Copolymer of THPMA and 1H,1H-Perfluorooctyl Methacrylate (F7MA). The procedure used was the same as that for the synthesis of block copolymers. However, both monomers were added simultaneously into the reaction chamber using two different syringes. Polymerization was continued for 6 h, and a milky solution was obtained, possibly due to the low solubility of the polymer in THF. Characterization. The number average molecular weights (Mns) and polydispersities of the copolymers were determined by GPC (THF) using PMMA as the standard, a Waters Associates 510 Pump, a 410 refractive index detector, and 4.6 mm × 300 mm Styragel HT3, HT4, HT5, and HT6E columns. The copolymer compositions were verified by 1H NMR studies carried out on a Varian 200 spectrometer using either CDCl3 or deuterated THF/CFCl3 as solvent. Compositions are reported in volume fractions rather than mole fractions, since these values are useful in predicting the microstructure of block copolymers. However, these values are estimates based on the experimentally measured density of the homopolymers (FTHPMA, 1.06; FF3MA, 1.4; FF7MA, 1.495; FHF4MA, 1.28). The glass transition temperatures of the copolymers were measured using differential scanning calorimetry (DSC) measurement on a Perkin-Elmer DSC-7 Series instrument at a 10 °C/min heating rate under nitrogen. Lithographic Processing. Polymer solutions for spincasting were prepared by dissolving 15-20 wt % of polymer in propylene glycol methyl ether acetate (PGMEA). Photoacid generators (PAGs) were added as needed. Photoacid generators of different polarities were used with different polymeric matrixes. Typical PAG concentrations in the polymer matrixes were 1-2 wt % of the polymer concentration in the solution. The solutions were then filtered using 0.2 or 0.45 µm PTFE filters. The polymer solutions were manually dispensed using an Eppendorf pipet. Approximately 2 mL of solution was needed to form a uniform film for each 8 in. silicon wafer. The silicon wafers were pretreated by one of two procedures: (1) vapor-priming with 1,1,1,3,3,3-hexamethyldisilazane (HMDS) at 120 °C for 25 s or (2) coating with Brewer Science DUV 18L antireflective coating and then baking at 120 °C for 25 s. Silicon wafers with the solution were then spun at appropriate speeds to obtain thin films of thickness ranging from 0.2 to 0.4 µm. The approximate range of speeds used was 1000-2000

Figure 3. Schematic of the supercritical CO2 development apparatus. rpm depending on the viscosity of the solutions. The samples were then baked at 120-150 °C for 60 s. Resist processing was done either at the Class 1 cleanroom facility at SEMATECH, Austin, TX, or at the experimental cleanroom facility at IBM Almaden Research Center, San Jose, CA. Reported exposures were made using a 193 nm ArF excimer laser source (SEMATECH, IBM Almaden). Both the 193-nm stepper at SEMATECH and that at IBM Almaden had a lens of variable numerical aperture (NA) of 0.6, a field size diameter of 1.5 mm × 1.5 mm, and a partial coherence of 0.7. Exposure dose matrixes were used to determine the sensitivities of the various photoresists. Typical dose matrixes ranged from 1 to 60 mJ/cm2 in steps of 1 mJ/cm2, although different ranges and steps were used depending on the photoresist. The postexposure bake was done at 120 or 90 °C for 60 s. Development of the photoresists was carried out in the in-house SCF CO2 resist-processing facility. The polymer film thickness after the postapply bake was determined using a Prometrix SM-200 film thickness probe. The Prometrix measures the film thickness using constant angle reflection interference spectroscopy (CARIS). It was assumed that the variation of the index of refraction with wavelength for some of the block copolymers was comparable to that for the corresponding homopolymer or random copolymer methacrylates of similar composition. The thickness of each of the films was averaged over 49 measurements covering the entire wafer. The films were very uniform with standard deviation